Refolding,purification and characterization of an organic solvent-tolerant lipase from Serratia marcescens ECU1010

Expression of recombinant proteins as inclusion bodies in bacteria is one of the most efficient ways to produce cloned proteins, as long as the inclusion bodies can be successfully refolded. In this study, the different parameters were investigated and optimized on the refolding of denatured lipase. The maximum lipase activity of 5000 U/L was obtained after incubation of denatured enzyme in a refolding buffer containing 20 mM Tris–HCl (pH 7.0), 1 mM Ca²⁺ at 20 °C. Then, the refolded lipase was purified to homogeneity by anion exchange chromatography. The purified refolded lipase was stable in broad ranges of temperatures and pH values, as well as in a series of water-miscible organic solvents. In addition, some water-immiscible organic solvents, such as petroleum ether and isopropyl ether, could reduce the polarity and increase the nonpolarity of the refolding system. The results of Fourier transform infrared (FT-IR) microspectroscopy were the first to confirm that lipase refolding could be further improved in the presence of organic solvents. The purified refolded lipase could enantioselectively hydrolyze trans-3-(4-methoxyphenyl) glycidic acid methyl ester [(±)-MPGM]. These features render the lipase attraction for biotechnological applications in the field of organic synthesis and pharmaceutical industry.     

Refolding of the immunoglobulin light chain.

The kinetics of the refolding reactions of type lambda Bence Jones proteins from 4 M GuHCl were studied by CD, ultraviolet absorption, and fluorescence spectrophotometry. The kinetics were complex and consisted of at least three phases, an undetectable fast phase, a detectable fast phase, and a slow phase. The slow phase followed first-order kinetics and the three experimental methods used gave similar rate constants for all the Bence Jones proteins (about 3 X 10(-3) s-1). The refolding reaction of VL fragment was too fast to be measured in the present experiments. The refolding process of CL fragment was very similar to those of Bence Jones proteins except that the detectable fast phase was less significant. The rate constant of the slow phase observed for the CL fragment was similar to those of the slow phase observed for Bence Jones proteins. The activation energy of the slow phase was the same for a Bence Jones protein and its CL fragment. These results indicate that the refolding kinetics of the CL domain are very similar to those of isolated CL fragment and that refolding of the VL domain precedes refolding of the CL domain, even though both domains have similar immunoglobulin folds. However, the results of refolding experiments on Bence Jones proteins, and VL and CL fragments in the presence of ANS, as well as the other lines of evidence, indicate that the refolding kinetics of the Bence Jones protein molecule cannot be expressed as simple sum of the refolding reactions of isolated VL and CL fragments.     

An Automatic Refolding Apparatus for Preparative-Scale Protein Production

Protein refolding is an important process to recover active recombinant proteins from inclusion bodies. Refolding by simple dilution, dialysis and on-column refolding methods are the most common techniques reported in the literature. However, the refolding process is time-consuming and laborious due to the variability of the behavior of each protein and requires a great deal of trial-and-error to achieve success. Hence, there is a need for automation to make the whole process as convenient as possible. In this study, we invented an automatic apparatus that integrated three refolding techniques: varying dilution, dialysis and on-column refolding. We demonstrated the effectiveness of this technology by varying the flow rates of the dilution buffer into the denatured protein and testing different refolding methods. We carried out different refolding methods on this apparatus: a combination of dilution and dialysis for human stromal cell-derived factor 1 (SDF-1/CXCL12) and thioredoxin fused-human artemin protein (Trx-ARTN); dilution refolding for thioredoxin fused-human insulin-like growth factor I protein (Trx-IGF1) and enhanced fluorescent protein (EGFP); and on-column refolding for bovine serum albumin (BSA). The protein refolding processes of these five proteins were preliminarily optimized using the slowly descending denaturants (or additives) method. Using this strategy of decreasing denaturants concentration, the efficiency of protein refolding was found to produce higher quantities of native protein. The standard refolding apparatus configuration can support different operations for different applications; it is not limited to simple dilution, dialysis and on-column refolding techniques. Refolding by slowly decreasing denaturants concentration, followed by concentration or purification on-column, may be a useful strategy for rapid and efficient recovery of active proteins from inclusion bodies. An automatic refolding apparatus employing this flexible strategy may provide a powerful tool for preparative scale protein production.     

Refolding of chemically denatured alpha-amylase in dilution additive mode

Cyclodextrins (CDs) possess hydrophobic surfaces, which probably shield the hydrophobic surfaces of denatured proteins and prevent the direct interactions between the surfaces which are believed to be responsible for protein aggregation during refolding process. This probability was evaluated by studying the refolding process of denatured alpha-amylase in the presence and absence of alpha-CD, as a dilution additive agent. Our data indicate that in the presence of 100 mM alpha-CD in the refolding buffer, the extent of aggregation reduces by almost 90%. Spectrofluorometric analysis of the refolding intermediate(s) also indicates that the tertiary structure of the refolded alpha-amylase, in the presence of alpha-CD, is very similar to the tertiary structure of the native protein. However, this similarity was distorted upon addition of exogenous hydrophobic (aliphatic or aromatic) amino acids to the refolding buffer, meaning that the hydrophobic interactions between alpha-CD and the denatured protein play significant role in preventing aggregate formation. In addition, by weakening the extent of these hydrophobic interactions by adding polarity-reducing agent (e.g. ethylene glycol) to the refolding buffer, more aggregates were formed. In contrast, strengthening these interactions by enhancing the ionic strength of the refolding buffer made these hydrophobic interactions very strong. Therefore, alpha-CD could not depart from the protein/alpha-CD complex, as it usually does during the process of refolding. As a result, more aggregates were formed in the presence of alpha-CD compared to the corresponding control samples.     

蛋白质的氧化重折叠

经过近几十年来广泛而深入的研究,蛋白质氧化重折叠的机制已得到相当详细的阐明。1在已研究过的蛋白质中,大多数蛋白质都是沿着多途径而非单一、特定的途径进行氧化重折叠,这与折叠能量景观学说是一致的。2正是氨基酸残基间的天然相互作用而不是非天然的相互作用控制蛋白质的折叠过程。这一结论与含非天然二硫键的折叠中间体在牛胰蛋白酶抑制剂（BPTI）折叠中所起的重要作用并非相互排斥,因为后者仅仅是进行链内二硫键重排的化学反应所必需,与控制肽链折叠无直接关系。3根据对BPTI的研究,二硫键曾被认为仅仅具有稳定蛋白质天然结构的作用,既不决定折叠途径也不决定其三维构象。这一观点不适用于其它蛋白质。对凝乳酶原的研究表明,天然二硫键的形成是恢复天然构象的前提。天然二硫键的形成与肽键的正确折叠相辅相成,更具有普遍意义。4在氧化重折叠的早期,二硫键的形成基本上是一个随机过程,随着肽链的折叠二硫键的形成越来越受折叠中间体构象的限制。提高重组蛋白质的复性产率是生物技术领域中的一个巨大的挑战。除了分子聚集外,在折叠过程中所形成的二硫键错配分子是导致低复性率的另一个主要原因。氧化重折叠机制的阐明为解决此问题提供了有益的启示。如上所述,在折叠的后期,二硫键的形成决定于折叠中间体的构象,类天然、有柔性的结构有利于天然二硫键形成和正确折叠,具有这类结构的分子为有效的折叠中间体,最终都能转变为天然产物;而无效折叠中间体往往具有稳定的结构,使巯基、二硫键内埋妨碍二硫键重排,并因能垒的障碍不利于进一步折叠。因此,降低无效折叠中间体的稳定性使之转变为有效折叠中间体是提高含二硫键蛋白质复性率的一条基本原则,实验证明,碱性pH、低温、降低蛋白质稳定性的试剂、蛋白质二硫键异构酶、改变蛋白质一级结构是实现这一原则的有效手段。此外,这里还就氧化重折叠的基础和应用研究的前景进行了讨论。     

Refolding process of cysteine-rich proteins:Chitinase as a model

Background:

Recombinant proteins overexpressed in E. coli are usually deposited in inclusion bodies. Cysteines in the protein contribute to this process. Inter- and intra- molecular disulfide bonds in chitinase, a cysteine-rich protein, cause aggregation when the recombinant protein is overexpressed in E. coli. Hence, aggregated proteins should be solubilized and allowed to refold to obtain native- or correctly- folded recombinant proteins.

Methods:

Dilution method that allows refolding of recombinant proteins, especially at high protein concentrations, is to slowly add the soluble protein to refolding buffer. For this purpose: first, the inclusion bodies containing insoluble proteins were purified; second, the aggregated proteins were solubilized; finally, the soluble proteins were refolded using glutathione redox system, guanidinium chloride, dithiothreitol, sucrose, and glycerol, simultaneously.

Results:

After protein solubilization and refolding, SDS-PAGE showed a 32 kDa band that was recognized by an anti-chitin antibody on western blots.

Conclusions:

By this method, cysteine-rich proteins from E. coli inclusion bodies can be solubilized and correctly folded into active proteins.Key Words: Chitinase, Cysteine-rich proteins, Protein refolding, Protein solubilization     

重组蛋白的体外再折叠

重组蛋白的再折叠是基因工程下游处理中非常重要的环节。本文在分析了蛋白体外折叠的机制后,指出了重组蛋白再折叠的一般策略,并综述了近年来的主要新方法,包括：分析伴侣介导的再折叠去污剂协助的再折叠,反向微团中的蛋白再折叠,折叠促进剂的添加以及再折地促进二硫键形成的方法 。     

Mutagenesis and characterization of specific residues in fatty acid ethyl ester synthase: A gene for alcohol-induced cardiomyopathy

Fatty acid ethyl ester synthase-III metabolizes both ethanol and carcinogens. Structure-function studies of the enzyme have not been performed in relation to site specific mutagenesis. In this study, three residues (Gly 32, Cys 39 and His 72) have been mutated to observe their role in enzyme activity. Gly to Gln, Cys to Trp and His to Ser mutations did not affect fatty acid ethyl ester synthase activity, but His to Ser mutant had less than 9% of control glutathione S-transferase activity. The apparent loss of transferase activity reflected a 28 fold weaker binding constant for glutathione. Thus, this study indicates that Gly and Cys may not be important for synthase or transferase activities however, histidine may play a role in glutathione binding, but it is not an essential catalytic residue of glutathione S-transferase or for fatty acid ethyl ester synthase activity.     

Site-specific mutagenesis of two histidine residues in fatty acid ethyl ester synthase-III.

Human myocardial fatty acid ethyl ester synthase-III is a newly described acidic glutathione S-transferase that metabolizes both ethanol and carcinogens. Structure-function studies have not been performed relating these two distinct enzymatic activities. Since there are only two histidine residues in fatty acid ethyl ester synthase-III (His 72 and His 163), the role of each was examined by site-specific mutagenesis. Fatty acid ethyl ester synthase-III mutagenized at position 72 to contain either Gln, Pro or Ala had less than 5% of control glutathione S-transferase activity but retained fatty acid ethyl ester synthase activity under standard assay conditions. In contrast, substitution of histidine 163 with proline had no effect on glutathione S-transferase activity, but it slightly increased synthase activity. Thus, this study indicates that histidine plays a differential role in fatty acid ethyl ester synthase III depending on the nucleophilic substrate.     

The Saccharomyces cerevisiae EHT1 and EEB1 genes encode novel enzymes with medium-chain fatty acid ethyl ester synthesis and hydrolysis capacity

Fatty acid ethyl esters are secondary metabolites produced by Saccharomyces cerevisiae and many other fungi. Their natural physiological role is not known but in fermentations of alcoholic beverages and other food products they play a key role as flavor compounds. Information about the metabolic pathways and enzymology of fatty acid ethyl ester biosynthesis, however, is very limited. In this work, we have investigated the role of a three-member S. cerevisiae gene family with moderately divergent sequences (YBR177c/EHT1, YPL095c/EEB1, and YMR210w). We demonstrate that two family members encode an acyl-coenzymeA:ethanol O-acyltransferase, an enzyme required for the synthesis of medium-chain fatty acid ethyl esters. Deletion of either one or both of these genes resulted in severely reduced medium-chain fatty acid ethyl ester production. Purified glutathione S-transferase-tagged Eht1 and Eeb1 proteins both exhibited acyl-coenzymeA:ethanol O-acyltransferase activity in vitro, as well as esterase activity. Overexpression of Eht1 and Eeb1 did not enhance medium-chain fatty acid ethyl ester content, which is probably due to the bifunctional synthesis and hydrolysis activity. Molecular modeling of Eht1 and Eeb1 revealed the presence of a alpha/beta-hydrolase fold, which is generally present in the substrate-binding site of esterase enzymes. Hence, our results identify Eht1 and Eeb1 as novel acyl-coenzymeA:ethanol O-acyltransferases/esterases, whereas the third family member, Ymr210w, does not seem to play an important role in medium-chain fatty acid ethyl ester formation.     

Refolding of Npro fusion proteins

The autoprotease N^pro significantly enhances expression of fused peptides and proteins and drives the formation of inclusion bodies during protein expression. Upon refolding, the autoprotease becomes active and cleaves itself specifically at its own C‐terminus releasing the target protein with its authentic N‐terminus. N^pro wild‐type and its mutant EDDIE, respectively, were fused N‐terminally to the model proteins green fluorescent protein, staphylococcus Protein A domain D, inhibitory peptide of senescence‐evasion‐factor, and the short 16 amino acid peptide pep6His. In comparison with the N^pro wild‐type, the tailored mutant EDDIE displayed an increased rate constant for refolding and cleavage from 1.3 × 10^?4 s^?1 to 3.5 × 10^?4 s^?1, and allowed a 15‐fold higher protein concentration of 1.1 mg/mL when studying pep6His as a fusion partner. For green fluorescent protein, the rate constant was increased from 2.4 × 10^?5 s^?1 to 1.1 × 10^?4 s^?1 when fused to EDDIE. When fused to small target peptides, refolding and cleavage yields were independent of initial protein concentration, even at high concentrations of 3.9 mg/mL, although cleavage rates were strongly influenced by the fusion partner. This behavior differed from conventional 1st order refolding kinetics, where yield strongly depends on initial protein concentration due to an aggregation reaction of higher order. Refolding and cleavage of EDDIE fusion proteins follow a monomolecular reaction for the autoproteolytic cleavage over a wide concentration range. At high protein concentrations, deviations from the model assumptions were observed and thus smaller rate constants were required to approximate the data. Biotechnol. Bioeng. 2009; 104: 774–784 © 2009 Wiley Periodicals, Inc.     

SOn-column Protein Refolding for Crystallization

One major bottleneck in protein production in Escherichia coli for structural genomics projects is the formation of insoluble protein aggregates (inclusion bodies). The efficient refolding of proteins from inclusion bodies is becoming an important tool that can provide soluble native proteins for structural and functional studies. Here we report an on-column refolding method established at the Berkeley Structural Genomics Center (BSGC). Our method is a combination of an ‘artificial chaperone-assisted refolding’ method previously proposed and affinity chromatography to take advantage of a chromatographic step: less time-consuming, no filtration or concentration, with the additional benefit of protein purification. It can be easily automated and formatted for high-throughput process.     

包涵体蛋白的分离和色谱法体外复性纯化研究进展

重组蛋白在大肠杆菌中表达多为无活性的包涵体形式,须经洗涤、溶解、复性后才能得到生物活性蛋白。综述了近年来包涵体蛋白分离纯化和复性技术研究进展,重点讨论了色谱法复性技术的应用,包括尺寸排阻色谱、亲和色谱、离子交换色谱、疏水相互作用色谱、固定化脂质体色谱、扩张床吸附色谱的进展情况。     

Ternary System of Solution Additives with Arginine and Salt for Refolding of Beta-Galactosidase

l-Arginine hydrochloride (Arg HCl) has been used for protein refolding as a universal aggregation suppressor for monomeric proteins. This paper presents an investigation of the refolding of tetrameric beta-galactosidase (β-gal) using Arg HCl and other salts. In a binary system using only Arg HCl, the refolding yield of β-gal increased with increasing concentration up to 0.2 M. However, the refolding yield sharply decreased above this concentration, reaching the level below the control yield of 5% at 0.5 M and near zero above 0.75 M, an observation unexpected from monomeric proteins. In a ternary system using both 0.2 M Arg HCl and another salt, the refolding yield increased up to 1.5-fold higher than that in the binary system. These data indicate that aggregation suppressive effects of protein increase with Arg HCl concentration, but also are deleterious to self-association of the protein. This dual nature of Arg HCl effects may have to be taken into account in its application for refolding of oligomeric proteins.     

重组包涵体蛋白质的折叠复性

综述了减少包涵体形成、包涵体分离和溶解以及包涵体折叠复性的策略及其最新进展 .详细讨论了包涵体蛋白质折叠复性的基本原则、包涵体折叠复性促进剂和包涵体折叠复性方法     

Oxidative refolding of rPA in l‐ArgHCl and in ionic liquids: A correlation between hydrophobicity,salt effects,and refolding yield

The ionic liquid 1‐ethyl‐3‐methyl imidazolium chloride (EMIM Cl) and the amino acid l‐ arginine hydrochloride (l ‐ArgHCl) have been successfully used to improve the yield of oxidative refolding for various proteins. However, the molecular mechanisms behind the actions of such solvent additives—especially of ionic liquids—are still not well understood. To analyze these mechanisms, we have determined the transfer free energies from water into ionic liquid solutions of proteinogenic amino acids and of diketopiperazine as peptide bond analogue. For EMIM Cl and 1‐ethyl‐3‐methyl imidazolium diethyl phosphate, which had a suppressive effect on protein refolding, as well as for l ‐ArgHCl favorable interactions with amino acid side chains, but no favorable interactions with the peptide backbone could be observed. A quantitative analysis of other ionic liquids together with their already published effects on protein refolding showed that only solvent additives within a certain range of hydrophobicity, chaotropicity and kosmotropicity were effective for the refolding of recombinant plasminogen activator. © 2014 Wiley Periodicals, Inc. Biopolymers 101: 1129–1140, 2014.     

Refolding of protein inclusion bodies directly from E. coli homogenate using expanded bed adsorption chromatography

To avoid the intrinsic problem of aggregation associated with the traditional solution-phase refolding process, we proposed a solid-phase refolding method integrated with the expanded bed adsorption chromatography. The model protein was a fusion protein of recombinant human growth hormone and a glutathione S-transferase fragment. It was demonstrated that the inclusion body proteins in the cell homogenate could be directly refolded with higher yield. To verify the applicability of this method, we have tested with success three types of the starting materials, i.e., rhGH monomer, inclusion bodies containing the fusion protein, and the E. coli cell homogenate. This direct refolding process could reduce the number of the renaturation steps required and allow the refolding at a higher concentration, approximately 2 mg fusion protein per ml resin. This revised version was published online in July 2006 with corrections to the Cover Date.     

蛋白质的排阻色谱复性的新进展

外源蛋白在大肠杆菌中高效表达时 ,常常形成不溶的、无活性的包涵体 ,包涵体蛋白的复性是重组蛋白生产过程中的一个技术难题。排阻色谱 (sizeexclusionchromatography ,SEC)用于蛋白复性是一种较新的、适用于任何一种蛋白的方法 ,与常用的稀释复性法相比 ,它能在高的起始蛋白浓度下对蛋白进行复性 ,活性回收率较高 ,同时又能使目标蛋白得到一定程度的纯化。对使用SEC复性的进展进行了评述 ,其内容包括SEC复性的原理及其复性过程中的影响因素 ,并对其未来发展进行了展望。     

Studies on the Refolding Process of Recombinant Horseradish Peroxidase

Horseradish peroxidase (HRP) is an important heme-containing glyco-enzyme that has been used in many biotechnological fields. Valuable proteins like HRP can be obtained in sufficient amounts using Escherichia coli as an expression system. However, frequently, the expression of recombinant enzyme results in inclusion bodies, and the refolding yield is generally low for proteins such as plant peroxidases. In this study, a recombinant HRP was cloned and expressed in the form of inclusion bodies. Initially, the influence of few additives on HRP refolding was assessed by the one factor at a time method. Subsequently, factors with significant effects including glycerol, GSSG/DTT, and the enzyme concentration were selected for further optimization by means of the central composite design of response surface methodology (RSM). Under the obtained optimal condition, refolding increased about twofold. The refolding process was then monitored by the intrinsic fluorescence intensity under optimal conditions (0.35 mM GSSG, 0.044 mM DTT, 7 % glycerol, 1.7 M urea, and 2 mM CaCl₂ in 20 mM Tris, pH 8.5) and the reconstitution of heme to the refolded peroxidase was detected by the Soret absorbance. Additionally, samples under unfolding and refolding conditions were analyzed by Zetasizer to determine size distribution in different media.     

Refolding intermediate of guanidine hydrochloride denatured aminoacylase

The refolding of aminoacylase denatured in 6M guanidine hydrochloride (GdnHCl) has been studied by measuring enzyme activity, fluorescence emission spectra, ANS fluorescence spectra and far-UV circular dichroism spectra. The results showed that GdnHCl-denatured aminoacylase could be refolded and reactivated by dilution. A refolding intermediate was observed for low concentrations of GdnHCl (between 0.5 and 1.2M). This refolding intermediate was characterized by an increased fluorescence emission intensity, a blue-shifted emission maximum, and by increased binding of the fluorescence probe 8-anilino-1-naphthalenesulfonate (ANS). The secondary structure of the intermediate was similar to that of the native enzyme, and was therefore quite similar to the molten globule state often found in the protein folding pathway. Combined with the previous evidence of existence of an intermediate during unfolding process, we therefore proposed that the unfolding and refolding of aminoacylase might share the same pathway. A comparison of the Apo-enzyme and Holo-enzyme showed that there was little effect of the zinc ion on the refolding of the aminoacylase. Our study, the first successful report of the refolding of this metalloenzyme, also showed that lowering the concentration and the temperature of the enzyme improved the refolding rate of aminoacylase. The system therefore provides a useful model to study the refolding of proteins with prosthetic groups.